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    Continuous catalyst regeneration reactor with a chamber for mixing gas and distributing gas in the oxychlorination zone
    5.
    发明授权
    Continuous catalyst regeneration reactor with a chamber for mixing gas and distributing gas in the oxychlorination zone 有权
    连续催化剂再生反应器，其具有用于混合气体并在氧氯化区中分配气体的室

    公开(公告)号：US09295985B2

    公开(公告)日：2016-03-29

    申请号：US13949340

    申请日：2013-07-24

    申请人： AXENS

    发明人： Xavier Decoodt ,  Cecile Plais ,  Frederic Bazer-Bachi

    IPC分类号： B01J38/44 ,  B01J23/96 ,  C10G35/24 ,  B01J8/12 ,  B01J23/42 ,  B01J27/13 ,  B01J27/32 ,  C10G35/12 ,  B01J27/135

    CPC分类号： B01J38/44 ,  B01J8/125 ,  B01J23/42 ,  B01J23/96 ,  B01J27/13 ,  B01J27/135 ,  B01J27/32 ,  B01J2219/00024 ,  C10G35/12 ,  C10G2400/02 ,  Y10T29/4973

    摘要： A reactor for regenerating catalyst grains comprises a vessel having an oxychlorination zone superimposed over a calcining zone having a line for introducing gas. A chamber, disposed between oxychlorination and calcining zones, comprises an internal space located between two plates which are gas tight and impervious to catalyst grains. A plurality of tubes pass through the chamber to allow catalyst to pass from oxychlorination zone to calcining zone. A plurality of means pass through the chamber to allow calcining gas to pass from calcining zone to oxychlorination zone. At least one oxychlorination gas injection line opens into the internal space of the chamber. Each means for passage of calcining gas comprises at least one orifice communicating with the chamber internal space, and a means for evacuating gas which is permeable to gas and impermeable to catalyst grains.

    摘要翻译： 用于再生催化剂颗粒的反应器包括具有叠加在具有用于引入气体的管线的煅烧区域上的氧氯化区的容器。 设置在氧氯化和煅烧区之间的室包括位于两个板之间的内部空间，其间气密和不透过催化剂颗粒。 多个管通过室以允许催化剂从氧氯化区通过到煅烧区。 多个装置通过该室以允许煅烧气体从煅烧区通过至氧氯化区。 至少一个氧氯化气注入管线通向腔室的内部空间。 用于通过煅烧气体的每个装置包括与腔室内部空间连通的至少一个孔口，以及用于排出气体的装置，该气体可渗透气体并且不可渗透到催化剂颗粒中。

    Processes for the continuous regeneration of a catalyst
    6.
    发明授权
    Processes for the continuous regeneration of a catalyst 有权
    催化剂连续再生的方法

    公开(公告)号：US09138738B1

    公开(公告)日：2015-09-22

    申请号：US14252237

    申请日：2014-04-14

    申请人： UOP LLC

    发明人： Bryan K. Glover ,  Ka Lok ,  Mary J. Wier ,  Mohamed S. Shakur ,  Michael A. Moore ,  Alexander Sabitov

    IPC分类号： B01J38/56 ,  B01J38/44 ,  B01J38/42 ,  B01J38/20 ,  B01J27/13 ,  B01J27/32

    CPC分类号： B01J38/44 ,  B01J27/13 ,  B01J27/32 ,  B01J38/20 ,  B01J38/42 ,  C10G35/085

    摘要： A process for regenerating a catalyst used in a reaction zone. In a regeneration zone, the catalyst may be cooled before passing into a chloride rich zone. The regeneration zone may also receive a heated ambient oxygen in a catalyst heating zone. The regeneration zone may also receive recovered chloride from a chloride recovering zone which removes and recovers chloride from regeneration gas taken from the regeneration zone. Heated ambient oxygen may also be introduced into a chlorination zone.

    摘要翻译： 用于再生反应区中使用的催化剂的方法。 在再生区中，催化剂可以在进入富氯化物区之前被冷却。 再生区也可以在催化剂加热区中接受加热的环境氧。 再生区还可以从氯化物回收区接收回收的氯化物，其从再生区取出并从再生气体中回收氯化物。 加热的环境氧也可以被引入氯化区。

    BF.sub.3 gas recovery process
    9.
    发明授权
    BF.sub.3 gas recovery process 失效
    BF3气体回收过程

    公开(公告)号：US5811616A

    公开(公告)日：1998-09-22

    申请号：US489880

    申请日：1995-06-13

    申请人： Richard A. Holub ,  Scott D. Soltis

    发明人： Richard A. Holub ,  Scott D. Soltis

    IPC分类号： B01J27/32 ,  C07C2/20 ,  C07C2/08 ,  C07C2/26

    CPC分类号： B01J27/32 ,  C07C2/20 ,  C07C2527/1213 ,  Y02P20/584

    摘要： BF.sub.3 is vaporized from specified crude polyolefin reaction product mixture in a vaporization zone at a temperature insufficient to decompose BF.sub.3 or any BF.sub.3 promoter complex in the mixture, and the vaporized BF.sub.3 may be recovered directly. Further, a process for the oligomerization of a liquid olefin composition and recovery of BF.sub.3 is described in which inert volatile material present in a liquid olefin composition is removed from the composition by vaporization, forming a degassed liquid olefin composition free of inert volatile material. The degassed liquid olefin composition is then contacted in a reaction zone with BF.sub.3 under conditions to oligomerize the olefin, forming crude polyolefin oligomerization reaction product mixture containing dissolved BF.sub.3, which may be treated as described.

    摘要翻译： BF 3在气化区内从指定的粗聚烯烃反应产物混合物中蒸发，其温度不足以分解混合物中的BF 3或任何BF 3助催化剂复合物，并且蒸发的BF 3可以直接回收。 此外，描述了液态烯烃组合物的低聚反应和BF 3的回收方法，其中存在于液态烯烃组合物中的惰性挥发性物质通过蒸发从组合物中除去，形成无惰性挥发性物质的脱气液体烯烃组合物。 然后脱气的液体烯烃组合物在反应区与BF 3在使烯烃低聚的条件下接触，形成含有溶解的BF 3的粗聚烯烃低聚反应产物混合物，其可以如上所述处理。

    Catalyst regeneration process
    10.
    发明授权
    Catalyst regeneration process 失效
    催化剂再生过程

    公开(公告)号：US5710326A

    公开(公告)日：1998-01-20

    申请号：US695165

    申请日：1991-05-03

    申请人： Carl R. Beck

    发明人： Carl R. Beck

    IPC分类号： B01J27/12 ,  B01J27/16 ,  B01J27/32 ,  C07B61/00 ,  C07C51/14

    CPC分类号： C07C51/14 ,  B01J27/32 ,  Y02P20/584

    摘要： A process for controlling the regeneration of boron trifluoride catalyst complexes in the production of carboxylic acids and other products using boron trifluoride hydrates as a catalyst. Catalyst strength is determined by measuring the electrical conductivity of the catalyst recovered from hydrolysis. If the conductivity is greater than a predetermined value, the hydrolysis water rate is reduced and if the conductivity is leas than a predetermined value, the hydrolysis water rate is increased. Conductivity is determined by a toroidal conductivity sensor and a control valve responsive to operation of the conductivity sensor serves to increase or decrease the flow rate accordingly.

    摘要翻译： 一种控制三氟化硼催化剂络合物在使用三氟化硼水合物作为催化剂的羧酸和其它产物生产中的再生方法。 通过测量从水解回收的催化剂的电导率来确定催化剂强度。 如果导电率大于预定值，则水解水的速率降低，如果电导率低于预定值，则水解水的速率增加。 电导率由环形电导率传感器确定，并且响应于电导率传感器的操作的控制阀用于相应地增加或减小流量。